WO2021136228A1 - Method for preparing copper ferrite/zeolite spinel composite material and use thereof - Google Patents
Method for preparing copper ferrite/zeolite spinel composite material and use thereof Download PDFInfo
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- WO2021136228A1 WO2021136228A1 PCT/CN2020/140597 CN2020140597W WO2021136228A1 WO 2021136228 A1 WO2021136228 A1 WO 2021136228A1 CN 2020140597 W CN2020140597 W CN 2020140597W WO 2021136228 A1 WO2021136228 A1 WO 2021136228A1
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- copper ferrite
- zeolite
- composite material
- copper
- spinel composite
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 118
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 118
- 239000010949 copper Substances 0.000 title claims abstract description 118
- 229910000859 α-Fe Inorganic materials 0.000 title claims abstract description 114
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 101
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 101
- 239000010457 zeolite Substances 0.000 title claims abstract description 101
- 229910052596 spinel Inorganic materials 0.000 title claims abstract description 64
- 239000011029 spinel Substances 0.000 title claims abstract description 64
- 239000002131 composite material Substances 0.000 title claims abstract description 59
- 238000000034 method Methods 0.000 title claims abstract description 23
- 238000003756 stirring Methods 0.000 claims abstract description 41
- MXWJVTOOROXGIU-UHFFFAOYSA-N atrazine Chemical compound CCNC1=NC(Cl)=NC(NC(C)C)=N1 MXWJVTOOROXGIU-UHFFFAOYSA-N 0.000 claims abstract description 35
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 31
- 239000000843 powder Substances 0.000 claims abstract description 29
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 22
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000003054 catalyst Substances 0.000 claims abstract description 10
- 230000003647 oxidation Effects 0.000 claims abstract description 10
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 10
- 229960004543 anhydrous citric acid Drugs 0.000 claims abstract description 9
- MVFCKEFYUDZOCX-UHFFFAOYSA-N iron(2+);dinitrate Chemical compound [Fe+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MVFCKEFYUDZOCX-UHFFFAOYSA-N 0.000 claims abstract 2
- 239000000203 mixture Substances 0.000 claims description 27
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 claims description 26
- 230000015556 catabolic process Effects 0.000 claims description 14
- 238000006731 degradation reaction Methods 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 229960004106 citric acid Drugs 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 abstract 3
- 238000001354 calcination Methods 0.000 abstract 1
- 239000000356 contaminant Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 11
- 230000003197 catalytic effect Effects 0.000 description 10
- 229910021538 borax Inorganic materials 0.000 description 6
- 239000007853 buffer solution Substances 0.000 description 6
- 239000004328 sodium tetraborate Substances 0.000 description 6
- 235000010339 sodium tetraborate Nutrition 0.000 description 6
- 229910021642 ultra pure water Inorganic materials 0.000 description 6
- 239000012498 ultrapure water Substances 0.000 description 6
- 238000006385 ozonation reaction Methods 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000575 pesticide Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002363 herbicidal effect Effects 0.000 description 2
- 239000004009 herbicide Substances 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 230000005389 magnetism Effects 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000003980 solgel method Methods 0.000 description 2
- JYEUMXHLPRZUAT-UHFFFAOYSA-N 1,2,3-triazine Chemical compound C1=CN=NN=C1 JYEUMXHLPRZUAT-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000282412 Homo Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 231100000693 bioaccumulation Toxicity 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 210000000750 endocrine system Anatomy 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 210000000987 immune system Anatomy 0.000 description 1
- -1 iron ions Chemical class 0.000 description 1
- 210000004324 lymphatic system Anatomy 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000036244 malformation Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 239000002420 orchard Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 210000004994 reproductive system Anatomy 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- BXDAOUXDMHXPDI-UHFFFAOYSA-N trifluoperazine hydrochloride Chemical compound [H+].[H+].[Cl-].[Cl-].C1CN(C)CCN1CCCN1C2=CC(C(F)(F)F)=CC=C2SC2=CC=CC=C21 BXDAOUXDMHXPDI-UHFFFAOYSA-N 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/33—Electric or magnetic properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/38—Organic compounds containing nitrogen
Definitions
- the invention relates to the technical field of water treatment, in particular to a preparation method and application of a copper ferrite/zeolite spinel composite material.
- the traditional advanced oxidation technology uses ⁇ OH as the main active substance to degrade pollutants.
- ⁇ OH has a strong oxidizing property and non-selectivity, which makes it react quickly with organic matter, and the oxidation rate constant is mostly 108M -1 s -1 ⁇ 1010M -1 s -1 .
- the heterogeneous catalytic ozonation process as one of the advanced oxidation technologies, is also based on promoting the decomposition of ozone to ⁇ OH to improve the removal of organic matter.
- the heterogeneous catalytic ozonation process does not require the addition of complex chemical agents to the reaction system, and the solid catalyst added to the reaction device is easy to recycle and process. At the same time, it has the characteristics of simple operation and convenient maintenance, so it has the advantages in the actual water treatment process. Good application prospects.
- Atrazine also known as atrazine, is a triazine pesticide herbicide. It is widely used in the control and prevention of weeds in corn, orchards and farmland. Due to its excellent herbicidal efficacy, low price and easy It has become one of the most widely used and most important herbicides in the world. my country is a large agricultural country. The production and use of pesticides are among the top in the world, accounting for about one-tenth of the world's total output. Atrazine has been used in my country since the early 1980s, and the scope of use has continued to expand in recent years.
- the invention provides a preparation method and application of a copper ferrite/zeolite spinel composite material, and prepares a practical, convenient and efficient catalyst, which can effectively catalyze the ozone oxidation and degradation of organic pollutant atrazine in water.
- the copper ferrite/zeolite spinel composite material is prepared by the impregnation-sol-gel method. Compared with a single ozone system, a single natural zeolite catalytic ozone system and a single copper ferrite catalytic ozone system, the copper ferrite/ The zeolite spinel composite material greatly improves the efficiency of ozone degradation of atrazine, and the degradation rate of atrazine is increased by about 30% within 40 minutes.
- the mass ratio of copper ferrite to natural zeolite powder is 1:1, it is prepared
- the copper ferrite/zeolite spinel composite material catalyzes the degradation of atrazine in water by ozonation, and completes the degradation in 120 minutes; and the copper ferrite/zeolite spinel composite material prepared by the present invention has stable performance and has stable performance after the reaction. Only 0.05mg/L ⁇ 0.09mg/L metal ions dissolve in the aqueous solution.
- the invention prepares the copper ferrite/zeolite spinel composite material, the preparation method is simple, the raw material price is low, it has strong magnetism, is easy to recycle, and can be reused.
- the invention can obtain the preparation method and application of the copper ferrite/zeolite spinel composite material.
- Figure 1 is a comparison diagram of the removal efficiency of atrazine in the 1# ⁇ 6# reactor in the comparative experiment, C 0 is the initial concentration of atrazine, and C t is the concentration of atrazine at any time t;
- ⁇ represents a single ozone system, ⁇ represents a single natural zeolite catalytic ozone system, ⁇ represents a single copper ferrite catalyzed ozone system, ⁇ represents a copper ferrite/zeolite spinel composite catalyzed ozone system prepared in Example 3,
- ⁇ represents an example Two prepared copper ferrite/zeolite spinel composite material catalytic ozone system, Representing the catalytic ozone system of the copper ferrite/zeolite spinel composite prepared in Example 1;
- Figure 2 is the copper ferrite/zeolite spinel composite material prepared in Example 1, the removal efficiency of atrazine in water within 0-120min, C 0 is the initial concentration of atrazine, and C t is A The concentration of Trazine at any time t, ⁇ represents the catalytic ozone system of the copper ferrite/zeolite spinel composite material prepared in Example 1.
- Specific embodiment 1 The preparation method of the copper ferrite/zeolite spinel composite material of this embodiment is completed in the following steps:
- the copper ferrite/zeolite spinel composite material is prepared by the impregnation-sol-gel method. Compared with a single ozone system, a single natural zeolite catalyzed ozone system, and a single copper ferrite catalyzed ozone system, the copper ferrite /Zolite spinel composite material greatly improves the efficiency of ozone degradation of atrazine, and the degradation rate of atrazine is increased by about 30% within 40 minutes.
- the mass ratio of copper ferrite to natural zeolite powder is 1:1, prepare The obtained copper ferrite/zeolite spinel composite material catalyzes the degradation of atrazine in water by ozonation, and completes the degradation in 120 minutes; and the copper ferrite/zeolite spinel composite material prepared in this embodiment has stable performance and is in the reaction Only 0.05mg/L ⁇ 0.09mg/L of metal ions dissolve in the aqueous solution.
- the copper ferrite/zeolite spinel composite material is prepared with simple preparation method, low raw material price, strong magnetism, easy recycling, and reusable use.
- this embodiment is different from specific embodiment one in that: in step one, under the temperature condition of 90°C ⁇ 100°C, copper nitrate and ferric nitrate are added to the absolute ethanol at 120r/min Stirring evenly at a stirring rate of ⁇ 180r/min.
- this embodiment is different from specific embodiment one or two in that: adding anhydrous citric acid as described in step one, and then stirring uniformly at a stirring rate of 120r/min ⁇ 180r/min to obtain copper ferrite sol State mixed liquid.
- this embodiment is different from one of specific embodiments one to three in that: in step two, under the temperature condition of 90°C ⁇ 100°C, the rate of 10mg/s ⁇ 20mg/s is added to copper ferrite Add natural zeolite powder to the sol mixed liquid, continue to stir at a stirring rate of 120r/min-180r/min until the copper ferrite sol mixed liquid evaporates to dryness.
- This embodiment is different from one of specific embodiments 1 to 4 in that: the natural zeolite powder described in step 2 is prepared in the following steps: natural zeolite with the same particle size is taken, crushed by a high-speed pulverizer, and then sequentially Wash with pure water and 0.1 mol/L hydrochloric acid to obtain natural zeolite powder.
- Embodiment 6 The difference between this embodiment and one of Embodiments 1 to 5 is: in step 2, the temperature is increased to 400° C. at a heating rate of 3° C./min, and it is calcined at 400° C. for 8 hours.
- Embodiment 7 The difference between this embodiment and Embodiments 1 to 6 is that the copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material described in step 2 has a particle size of 2 ⁇ m ⁇ 30 ⁇ m.
- Embodiment 8 This embodiment is different from one of Embodiments 1 to 7 in that the mass ratio of copper ferrite to natural zeolite powder in the copper ferrite sol mixed liquid in step 2 is 1:1.
- Specific embodiment 9 Application of copper ferrite/zeolite spinel composite material.
- the copper ferrite/zeolite spinel composite material is used as a catalyst to catalyze ozone oxidation and degradation of atrazine in water.
- Embodiment 10 This embodiment is different from Embodiment 9 in that: when the copper ferrite/zeolite spinel composite material is used as a catalyst, the addition amount is 0.05 g/L to 1.0 g/L.
- Example 1 The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
- the copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material has a particle size of 2 ⁇ m to 30 ⁇ m, and the copper ferrite sol-state mixture contains the copper ferrite and natural zeolite The mass ratio of powder is 1:1.
- the natural zeolite powder described in step two is prepared according to the following steps: natural zeolite with uniform particle size is taken, crushed by a high-speed pulverizer, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
- Embodiment 2 The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
- the copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material has a particle size of 2 ⁇ m-30 ⁇ m, and the copper ferrite sol-state mixture contains the copper ferrite and natural zeolite The mass ratio of powder is 1:2.
- the natural zeolite powder described in step two is prepared according to the following steps: natural zeolite with uniform particle size is taken, crushed by a high-speed pulverizer, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
- Example 3 The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
- the copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material has a particle size of 2 ⁇ m to 30 ⁇ m, and the copper ferrite sol-state mixture contains the copper ferrite and natural zeolite
- the mass ratio of powder is 1:5.
- the natural zeolite powder described in step two is prepared according to the following steps: natural zeolite with uniform particle size is taken, crushed by a high-speed pulverizer, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
- Figure 1 is a comparison diagram of the removal efficiency of atrazine in the 1# ⁇ 6# reactor in the comparative test; as shown in Figure 1, it is the same as a single ozone system, a single natural zeolite catalyzed ozone system and a single copper ferrite catalyzed ozone Compared with the system, the copper ferrite/zeolite spinel composite materials prepared in Example 1 to Example 3 show very high catalytic activity. Within 40 minutes of reaction time, the removal rate of atrazine in water is relatively high. The effect of ozone is increased by about 30%, and it has high chemical stability. Only trace amounts of copper and iron ions are detected in the aqueous solution after the reaction, which can be used in the actual water treatment field.
- the copper ferrite/zeolite catalyst has no obvious adsorption effect; and the ozone oxidation alone can only degrade a small amount of atrazine; therefore, the copper ferrite/zeolite spinel composite material prepared in Examples 1 to 3 is made Simple, low cost, simple operation and high catalytic efficiency.
- Figure 2 is a graph showing the removal efficiency of atrazine from water in the copper ferrite/zeolite spinel composite material prepared in Example 1 within 0 to 120 minutes; as shown in Figure 2, the copper ferrite/zeolite spinel composite material prepared in Example 1 The zeolite spinel composite material completely degrades the atrazine in the water at 120 minutes.
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Abstract
Disclosed are a method for preparing a copper ferrite/zeolite spinel composite material and the use thereof, which relates to the technical field of water treatment. The present invention provides a method for preparing a copper ferrite/zeolite spinel composite material, and the use thereof, and thus, a practical, convenient and efficient catalyst is prepared, which catalyst can effectively catalyze ozone oxidation so as to degrade an organic contaminant, atrazine, in water. The method comprises: adding copper nitrate and iron nitrate to anhydrous ethanol, stirring same, then adding anhydrous citric acid, and then stirring same to obtain a copper ferrite mixed solution in a sol state; and adding a natural zeolite powder into the copper ferrite mixed solution in a sol state, continuing stirring until the copper ferrite mixed solution in a sol state is evaporated to dryness, then grinding same, then calcining same at a high temperature, and finally, air cooling same to room temperature and grinding same to obtain the copper ferrite/zeolite spinel composite material. By means of the present invention, a method for preparing a copper ferrite/zeolite spinel composite material and the use thereof can be obtained.
Description
本发明涉及水处理技术领域,具体涉及铁酸铜/沸石尖晶石复合材料的制备方法及其应用。The invention relates to the technical field of water treatment, in particular to a preparation method and application of a copper ferrite/zeolite spinel composite material.
传统的高级氧化技术是以·OH为主要活性物质降解污染物。·OH具有极强的氧化性和无选择性,使得它与有机物反应速度很快,氧化速率常数大多在108M
-1s
-1~1010M
-1s
-1。非均相催化臭氧氧化工艺作为高级氧化技术之一,也是以促进臭氧分解为·OH为主,从而来提高有机物的去除效果。非均相催化臭氧氧化工艺不需要向反应体系中加入复杂的化学药剂,并且加入到反应装置的固体催化剂易于回收处理,同时具有操作运行简单、维护方便等特点,因此在实际水处理过程中具有良好的应用前景。
The traditional advanced oxidation technology uses ·OH as the main active substance to degrade pollutants. ·OH has a strong oxidizing property and non-selectivity, which makes it react quickly with organic matter, and the oxidation rate constant is mostly 108M -1 s -1 ~1010M -1 s -1 . The heterogeneous catalytic ozonation process, as one of the advanced oxidation technologies, is also based on promoting the decomposition of ozone to ·OH to improve the removal of organic matter. The heterogeneous catalytic ozonation process does not require the addition of complex chemical agents to the reaction system, and the solid catalyst added to the reaction device is easy to recycle and process. At the same time, it has the characteristics of simple operation and convenient maintenance, so it has the advantages in the actual water treatment process. Good application prospects.
阿特拉津(Atrazine,ATZ)又名莠去津,是一种三嗪类农药除草剂,被广泛应用于玉米、果园及农田杂草的控制和防治,由于其除草功效优良、价廉易得,成为目前世界上使用最广泛也是最重要的除草剂之一。我国是一个农业大国,农药的生产与使用均居世界前列,约占世界总产量的十分之一。我国从上个世纪80年代初开始使用阿特拉津,近年来使用范围仍不断扩大。研究表明,在所施用的农药中,有20%~70%会长期残留于土壤中,而阿特拉津具有土壤淋溶性,容易经降雨或地表水淋滤渗入含水层内产生生物富集,引起水环境污染。人体长期暴露在阿特拉津中,免疫系统、淋巴系统、生殖系统和内分泌系统都会受到影响,有可能产生畸形、诱导有机体突变等,严重危害人类健康。因此,开发有效的处理技术以去除水中的阿特拉津至关重要。Atrazine (ATZ), also known as atrazine, is a triazine pesticide herbicide. It is widely used in the control and prevention of weeds in corn, orchards and farmland. Due to its excellent herbicidal efficacy, low price and easy It has become one of the most widely used and most important herbicides in the world. my country is a large agricultural country. The production and use of pesticides are among the top in the world, accounting for about one-tenth of the world's total output. Atrazine has been used in my country since the early 1980s, and the scope of use has continued to expand in recent years. Studies have shown that 20% to 70% of the pesticides applied will remain in the soil for a long time, and atrazine has soil leaching properties, which can easily penetrate into the aquifer through rainfall or surface water leaching to produce bioaccumulation. Cause water pollution. If the human body is exposed to atrazine for a long time, the immune system, lymphatic system, reproductive system and endocrine system will be affected, which may cause malformations and induce organism mutations, which will seriously endanger human health. Therefore, it is important to develop effective treatment technologies to remove atrazine from the water.
阿特拉津的降解脱除主要有以下三种方法:物理吸附,化学氧化和生物降解,但是以上方法存在普遍成本高、实验过程慢和阿特拉津降解不完全的问题。使用吸附法,经济有效的吸附剂制备比较困难,此外还存在解析的问题;采用氧化法,工艺的运行处理费用较高,在一定程度上限制了它们的推广;利用微生物降解,存在是否会产生二次污染、微生物是否会释放出对人类有害的物质等担忧。There are three main methods for the degradation and removal of atrazine: physical adsorption, chemical oxidation and biodegradation, but the above methods have the problems of high cost, slow experimental process and incomplete degradation of atrazine. Using the adsorption method, it is difficult to prepare cost-effective adsorbents, and there are also analytical problems; the oxidation method is used, and the operation and treatment costs of the process are high, which limits their promotion to a certain extent; whether the use of microbial degradation will produce Concerns about secondary pollution and whether microorganisms will release substances harmful to humans.
发明内容Summary of the invention
本发明提供铁酸铜/沸石尖晶石复合材料的制备方法及其应用,制备得到一种实用、方便且高效的催化剂,能够有效地催化臭氧氧化降解水体中的有机污染物阿特拉津。The invention provides a preparation method and application of a copper ferrite/zeolite spinel composite material, and prepares a practical, convenient and efficient catalyst, which can effectively catalyze the ozone oxidation and degradation of organic pollutant atrazine in water.
铁酸铜/沸石尖晶石复合材料的制备方法,按以下步骤完成:The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
一、在90℃~100℃的温度条件下,将硝酸铜和硝酸铁加入到无水乙醇中,搅拌均匀,然后加入无水柠檬酸,再搅拌均匀,得到铁酸铜溶胶态混合液,所述硝酸铜与硝酸铁的摩尔比为1:2,硝酸铜和硝酸铁的总物质的量与无水乙醇的体积的比为11.49mmol:(100mL~120mL),无水乙醇的体积与无水柠檬酸的物质的量的比为(100mL~120mL):7.66mmol;1. Under the temperature condition of 90℃~100℃, add copper nitrate and ferric nitrate to absolute ethanol, stir evenly, then add anhydrous citric acid, and stir evenly to obtain copper ferrite sol state mixture, so The molar ratio of copper nitrate to ferric nitrate is 1:2, the ratio of the total amount of copper nitrate and ferric nitrate to the volume of absolute ethanol is 11.49mmol: (100mL~120mL), the volume of absolute ethanol is relative to that of anhydrous ethanol. The ratio of the amount of citric acid is (100mL~120mL): 7.66mmol;
二、在90℃~100℃的温度条件下,以10mg/s~20mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续搅拌至铁酸铜溶胶态混合液蒸干,然后进行研磨,再升温至400℃,并在400℃的温度条件下煅烧8h,最后空冷至室温,研磨,得到铁酸铜/沸石尖晶石复合材料,所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:(1~5)。2. Under the temperature condition of 90℃~100℃, add natural zeolite powder to the copper ferrite sol mixture at a rate of 10mg/s~20mg/s, and continue to stir until the copper ferrite sol mixture is evaporated to dryness. Then it was ground, heated to 400°C, and calcined at 400°C for 8 hours, and finally cooled to room temperature in air, and ground to obtain a copper ferrite/zeolite spinel composite material. The copper ferrite sol-state mixture contained iron The mass ratio of acid copper to natural zeolite powder is 1:(1~5).
本发明的有益效果:The beneficial effects of the present invention:
一、本发明通过浸渍-溶胶凝胶法制备铁酸铜/沸石尖晶石复合材料,与单独臭氧体系、单独天然沸石催化臭氧体系和单独铁酸铜催化臭氧体系相比,该铁酸铜/沸石尖晶石复合材料大大提高臭氧降解阿特拉津的效率,40分钟内阿特拉津降解率提升约30%,当铁酸铜与天然沸石粉的质量比为1:1时,制备得到的铁酸铜/沸石尖晶石复合材料催化臭氧氧化降解水中的阿特拉津,120min达完全降解;并且本发明制备的铁酸铜/沸石尖晶石复合材料,性能稳定,在反应后的水溶液中只有0.05mg/L~0.09mg/L的金属离子溶出。1. In the present invention, the copper ferrite/zeolite spinel composite material is prepared by the impregnation-sol-gel method. Compared with a single ozone system, a single natural zeolite catalytic ozone system and a single copper ferrite catalytic ozone system, the copper ferrite/ The zeolite spinel composite material greatly improves the efficiency of ozone degradation of atrazine, and the degradation rate of atrazine is increased by about 30% within 40 minutes. When the mass ratio of copper ferrite to natural zeolite powder is 1:1, it is prepared The copper ferrite/zeolite spinel composite material catalyzes the degradation of atrazine in water by ozonation, and completes the degradation in 120 minutes; and the copper ferrite/zeolite spinel composite material prepared by the present invention has stable performance and has stable performance after the reaction. Only 0.05mg/L~0.09mg/L metal ions dissolve in the aqueous solution.
二、本发明制备铁酸铜/沸石尖晶石复合材料,制备方法简单,原材料价格低廉,具有强磁性,易回收,可重复使用。2. The invention prepares the copper ferrite/zeolite spinel composite material, the preparation method is simple, the raw material price is low, it has strong magnetism, is easy to recycle, and can be reused.
本发明可获得铁酸铜/沸石尖晶石复合材料的制备方法及其应用。The invention can obtain the preparation method and application of the copper ferrite/zeolite spinel composite material.
图1为对比试验中,1#~6#反应器中阿特拉津的去除效率的对比图,C
0为阿特拉津的初始浓度,C
t为阿特拉津任意t时刻的浓度;■代表单独臭氧体系,●代表单独天然沸石催化臭氧体系,▲代表单独铁酸铜催化臭氧体系,▼代表实施例三制备的铁酸铜/沸石尖晶石复合材料催化臭氧体系,◆代表实施例二制备的铁酸铜/沸石尖晶石复合材料催化臭氧体系,
代表实施例一制备的铁酸铜/沸石尖晶石复合材料催化臭氧体系;
Figure 1 is a comparison diagram of the removal efficiency of atrazine in the 1#~6# reactor in the comparative experiment, C 0 is the initial concentration of atrazine, and C t is the concentration of atrazine at any time t; ■ represents a single ozone system, ● represents a single natural zeolite catalytic ozone system, ▲ represents a single copper ferrite catalyzed ozone system, ▼ represents a copper ferrite/zeolite spinel composite catalyzed ozone system prepared in Example 3, ◆ represents an example Two prepared copper ferrite/zeolite spinel composite material catalytic ozone system, Representing the catalytic ozone system of the copper ferrite/zeolite spinel composite prepared in Example 1;
图2为实施例一制备的铁酸铜/沸石尖晶石复合材料,在0~120min内对水中阿特拉津的去除效率图,C
0为阿特拉津的初始浓度,C
t为阿特拉津任意t时刻的浓度,■代表实施例一制备的铁酸铜/沸石尖晶石复合材料催化臭氧体系。
Figure 2 is the copper ferrite/zeolite spinel composite material prepared in Example 1, the removal efficiency of atrazine in water within 0-120min, C 0 is the initial concentration of atrazine, and C t is A The concentration of Trazine at any time t, ■ represents the catalytic ozone system of the copper ferrite/zeolite spinel composite material prepared in Example 1.
具体实施方式一:本实施方式铁酸铜/沸石尖晶石复合材料的制备方法,按以下步骤 完成:Specific embodiment 1: The preparation method of the copper ferrite/zeolite spinel composite material of this embodiment is completed in the following steps:
一、在90℃~100℃的温度条件下,将硝酸铜和硝酸铁加入到无水乙醇中,搅拌均匀,然后加入无水柠檬酸,再搅拌均匀,得到铁酸铜溶胶态混合液,所述硝酸铜与硝酸铁的摩尔比为1:2,硝酸铜和硝酸铁的总物质的量与无水乙醇的体积的比为11.49mmol:(100mL~120mL),无水乙醇的体积与无水柠檬酸的物质的量的比为(100mL~120mL):7.66mmol;1. Under the temperature condition of 90℃~100℃, add copper nitrate and ferric nitrate to absolute ethanol, stir evenly, then add anhydrous citric acid, and stir evenly to obtain copper ferrite sol state mixture, so The molar ratio of copper nitrate to ferric nitrate is 1:2, the ratio of the total amount of copper nitrate and ferric nitrate to the volume of anhydrous ethanol is 11.49mmol: (100mL~120mL), the volume of anhydrous ethanol is relative to that of anhydrous ethanol. The ratio of the amount of citric acid is (100mL~120mL): 7.66mmol;
二、在90℃~100℃的温度条件下,以10mg/s~20mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续搅拌至铁酸铜溶胶态混合液蒸干,然后进行研磨,再升温至400℃,并在400℃的温度条件下煅烧8h,最后空冷至室温,研磨,得到铁酸铜/沸石尖晶石复合材料,所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:(1~5)。2. Under the temperature condition of 90℃~100℃, add natural zeolite powder to the copper ferrite sol mixture at a rate of 10mg/s~20mg/s, and continue to stir until the copper ferrite sol mixture is evaporated to dryness. Then it was ground, heated to 400°C, and calcined at 400°C for 8 hours, and finally cooled to room temperature in air, and ground to obtain a copper ferrite/zeolite spinel composite material. The copper ferrite sol-state mixture contained iron The mass ratio of acid copper to natural zeolite powder is 1:(1~5).
本实施方式的有益效果:The beneficial effects of this embodiment:
一、本实施方式通过浸渍-溶胶凝胶法制备铁酸铜/沸石尖晶石复合材料,与单独臭氧体系、单独天然沸石催化臭氧体系和单独铁酸铜催化臭氧体系相比,该铁酸铜/沸石尖晶石复合材料大大提高臭氧降解阿特拉津的效率,40分钟内阿特拉津降解率提升约30%,当铁酸铜与天然沸石粉的质量比为1:1时,制备得到的铁酸铜/沸石尖晶石复合材料催化臭氧氧化降解水中的阿特拉津,120min达完全降解;并且本实施方式制备的铁酸铜/沸石尖晶石复合材料,性能稳定,在反应后的水溶液中只有0.05mg/L~0.09mg/L的金属离子溶出。1. In this embodiment, the copper ferrite/zeolite spinel composite material is prepared by the impregnation-sol-gel method. Compared with a single ozone system, a single natural zeolite catalyzed ozone system, and a single copper ferrite catalyzed ozone system, the copper ferrite /Zolite spinel composite material greatly improves the efficiency of ozone degradation of atrazine, and the degradation rate of atrazine is increased by about 30% within 40 minutes. When the mass ratio of copper ferrite to natural zeolite powder is 1:1, prepare The obtained copper ferrite/zeolite spinel composite material catalyzes the degradation of atrazine in water by ozonation, and completes the degradation in 120 minutes; and the copper ferrite/zeolite spinel composite material prepared in this embodiment has stable performance and is in the reaction Only 0.05mg/L~0.09mg/L of metal ions dissolve in the aqueous solution.
二、本实施方式制备铁酸铜/沸石尖晶石复合材料,制备方法简单,原材料价格低廉,具有强磁性,易回收,可重复使用。2. In this embodiment, the copper ferrite/zeolite spinel composite material is prepared with simple preparation method, low raw material price, strong magnetism, easy recycling, and reusable use.
具体实施方式二:本实施方式与具体实施方式一不同点是:步骤一中所述在90℃~100℃的温度条件下,将硝酸铜和硝酸铁加入到无水乙醇中,以120r/min~180r/min的搅拌速率搅拌均匀。Specific embodiment two: this embodiment is different from specific embodiment one in that: in step one, under the temperature condition of 90℃~100℃, copper nitrate and ferric nitrate are added to the absolute ethanol at 120r/min Stirring evenly at a stirring rate of ~180r/min.
其他步骤与具体实施方式一相同。The other steps are the same as in the first embodiment.
具体实施方式三:本实施方式与具体实施方式一或二不同点是:步骤一中所述加入无水柠檬酸,再以120r/min~180r/min的搅拌速率搅拌均匀,得到铁酸铜溶胶态混合液。Specific embodiment three: this embodiment is different from specific embodiment one or two in that: adding anhydrous citric acid as described in step one, and then stirring uniformly at a stirring rate of 120r/min~180r/min to obtain copper ferrite sol State mixed liquid.
其他步骤与具体实施方式一或二相同。The other steps are the same as the first or second embodiment.
具体实施方式四:本实施方式与具体实施方式一至三之一不同点是:步骤二中所述在90℃~100℃的温度条件下,以10mg/s~20mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续以120r/min~180r/min的搅拌速率搅拌至铁酸铜溶胶态混合液蒸干。Specific embodiment four: this embodiment is different from one of specific embodiments one to three in that: in step two, under the temperature condition of 90℃~100℃, the rate of 10mg/s~20mg/s is added to copper ferrite Add natural zeolite powder to the sol mixed liquid, continue to stir at a stirring rate of 120r/min-180r/min until the copper ferrite sol mixed liquid evaporates to dryness.
其他步骤与具体实施方式一至三相同。The other steps are the same as those in the first to third specific embodiments.
具体实施方式五:本实施方式与具体实施方式一至四之一不同点是:步骤二中所述的天然沸石粉按以下步骤制备:取粒径一致的天然沸石,经高速粉碎机粉碎,然后依次用纯水和0.1mol/L盐酸清洗,得到天然沸石粉。Specific embodiment five: This embodiment is different from one of specific embodiments 1 to 4 in that: the natural zeolite powder described in step 2 is prepared in the following steps: natural zeolite with the same particle size is taken, crushed by a high-speed pulverizer, and then sequentially Wash with pure water and 0.1 mol/L hydrochloric acid to obtain natural zeolite powder.
其他步骤与具体实施方式一至四相同。The other steps are the same as those in the first to fourth specific embodiments.
具体实施方式六:本实施方式与具体实施方式一至五之一不同点是:步骤二中所述再以3℃/min的升温速率升温至400℃,并在400℃的温度条件下煅烧8h。Embodiment 6: The difference between this embodiment and one of Embodiments 1 to 5 is: in step 2, the temperature is increased to 400° C. at a heating rate of 3° C./min, and it is calcined at 400° C. for 8 hours.
其他步骤与具体实施方式一至五相同。The other steps are the same as those in the first to fifth specific embodiments.
具体实施方式七:本实施方式与具体实施方式一至六之一不同点是:步骤二中所述的铁酸铜/沸石尖晶石复合材料上负载的铁酸铜尖晶石的粒径为2μm~30μm。Embodiment 7: The difference between this embodiment and Embodiments 1 to 6 is that the copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material described in step 2 has a particle size of 2 μm ~30μm.
其他步骤与具体实施方式一至六相同。The other steps are the same as those in the first to sixth specific embodiments.
具体实施方式八:本实施方式与具体实施方式一至七之一不同点是:步骤二中所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:1。Embodiment 8: This embodiment is different from one of Embodiments 1 to 7 in that the mass ratio of copper ferrite to natural zeolite powder in the copper ferrite sol mixed liquid in step 2 is 1:1.
其他步骤与具体实施方式一至七相同。The other steps are the same as in the first to seventh specific embodiments.
具体实施方式九:铁酸铜/沸石尖晶石复合材料的应用,所述铁酸铜/沸石尖晶石复合材料作为催化剂,用于催化臭氧氧化降解水中的阿特拉津。Specific embodiment 9: Application of copper ferrite/zeolite spinel composite material. The copper ferrite/zeolite spinel composite material is used as a catalyst to catalyze ozone oxidation and degradation of atrazine in water.
具体实施方式十:本实施方式与具体实施方式九不同点是:所述铁酸铜/沸石尖晶石复合材料作为催化剂时,添加量为0.05g/L~1.0g/L。Embodiment 10: This embodiment is different from Embodiment 9 in that: when the copper ferrite/zeolite spinel composite material is used as a catalyst, the addition amount is 0.05 g/L to 1.0 g/L.
其他步骤与具体实施方式九相同。The other steps are the same as in the ninth embodiment.
采用以下实施例验证本发明的有益效果:The following examples are used to verify the beneficial effects of the present invention:
实施例一:铁酸铜/沸石尖晶石复合材料的制备方法,按以下步骤完成:Example 1: The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
一、将120mL无水乙醇置于水浴锅中,在95℃的温度条件下,将3.83mmol硝酸铜和7.66mmol硝酸铁加入到120mL无水乙醇中,以180r/min的搅拌速率搅拌均匀,然后加入7.66mmol无水柠檬酸,再以180r/min的搅拌速率搅拌均匀,得到铁酸铜溶胶态混合液;1. Put 120mL of absolute ethanol in a water bath, add 3.83mmol copper nitrate and 7.66mmol ferric nitrate to 120mL of absolute ethanol at a temperature of 95°C, stir evenly at a stirring rate of 180r/min, and then Add 7.66mmol of anhydrous citric acid, and then stir evenly at a stirring rate of 180r/min to obtain a copper ferrite sol-state mixture;
二、在95℃的温度条件下,以10mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续以180r/min的搅拌速率搅拌至铁酸铜溶胶态混合液蒸干,然后进行研磨,再置于马弗炉中,以3℃/min的升温速率升温至400℃,并在400℃的温度条件下煅烧8h,最后空冷至室温,研磨,得到铁酸铜/沸石尖晶石复合材料,所述的铁酸铜/沸石尖晶石复合材料上负载的铁酸铜尖晶石的粒径为2μm~30μm,所述铁酸铜溶胶态混合液中铁酸铜与天 然沸石粉的质量比为1:1。2. Under the temperature condition of 95℃, add natural zeolite powder to the copper ferrite sol mixture at a rate of 10mg/s, and continue to stir at a stirring rate of 180r/min until the copper ferrite sol mixture is evaporated to dryness. Then it was ground, placed in a muffle furnace, heated to 400°C at a heating rate of 3°C/min, and calcined at 400°C for 8 hours, finally cooled to room temperature in air, and ground to obtain copper ferrite/zeolite tip The copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material has a particle size of 2 μm to 30 μm, and the copper ferrite sol-state mixture contains the copper ferrite and natural zeolite The mass ratio of powder is 1:1.
步骤二中所述的天然沸石粉按以下步骤制备:取粒径一致的天然沸石,经高速粉碎机粉碎,然后依次用纯水和0.1mol/L盐酸清洗,得到天然沸石粉。The natural zeolite powder described in step two is prepared according to the following steps: natural zeolite with uniform particle size is taken, crushed by a high-speed pulverizer, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
实施例二:铁酸铜/沸石尖晶石复合材料的制备方法,按以下步骤完成:Embodiment 2: The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
一、将120mL无水乙醇置于水浴锅中,在95℃的温度条件下,将3.83mmol硝酸铜和7.66mmol硝酸铁加入到120mL无水乙醇中,以180r/min的搅拌速率搅拌均匀,然后加入7.66mmol无水柠檬酸,再以180r/min的搅拌速率搅拌均匀,得到铁酸铜溶胶态混合液;1. Put 120mL of absolute ethanol in a water bath, add 3.83mmol copper nitrate and 7.66mmol ferric nitrate to 120mL of absolute ethanol at a temperature of 95°C, stir evenly at a stirring rate of 180r/min, and then Add 7.66mmol of anhydrous citric acid, and then stir evenly at a stirring rate of 180r/min to obtain a copper ferrite sol-state mixture;
二、在95℃的温度条件下,以10mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续以180r/min的搅拌速率搅拌至铁酸铜溶胶态混合液蒸干,然后进行研磨,再置于马弗炉中,以3℃/min的升温速率升温至400℃,并在400℃的温度条件下煅烧8h,最后空冷至室温,研磨,得到铁酸铜/沸石尖晶石复合材料,所述的铁酸铜/沸石尖晶石复合材料上负载的铁酸铜尖晶石的粒径为2μm~30μm,所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:2。2. Under the temperature condition of 95℃, add natural zeolite powder to the copper ferrite sol mixture at a rate of 10mg/s, and continue to stir at a stirring rate of 180r/min until the copper ferrite sol mixture is evaporated to dryness. Then it was ground, placed in a muffle furnace, heated to 400°C at a heating rate of 3°C/min, and calcined at 400°C for 8 hours, finally cooled to room temperature in air, and ground to obtain copper ferrite/zeolite tip The copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material has a particle size of 2 μm-30 μm, and the copper ferrite sol-state mixture contains the copper ferrite and natural zeolite The mass ratio of powder is 1:2.
步骤二中所述的天然沸石粉按以下步骤制备:取粒径一致的天然沸石,经高速粉碎机粉碎,然后依次用纯水和0.1mol/L盐酸清洗,得到天然沸石粉。The natural zeolite powder described in step two is prepared according to the following steps: natural zeolite with uniform particle size is taken, crushed by a high-speed pulverizer, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
实施例三:铁酸铜/沸石尖晶石复合材料的制备方法,按以下步骤完成:Example 3: The preparation method of copper ferrite/zeolite spinel composite material is completed according to the following steps:
一、将120mL无水乙醇置于水浴锅中,在95℃的温度条件下,将3.83mmol硝酸铜和7.66mmol硝酸铁加入到120mL无水乙醇中,以180r/min的搅拌速率搅拌均匀,然后加入7.66mmol无水柠檬酸,再以180r/min的搅拌速率搅拌均匀,得到铁酸铜溶胶态混合液;1. Put 120mL of absolute ethanol in a water bath, add 3.83mmol copper nitrate and 7.66mmol ferric nitrate to 120mL of absolute ethanol at a temperature of 95°C, stir evenly at a stirring rate of 180r/min, and then Add 7.66mmol of anhydrous citric acid, and then stir evenly at a stirring rate of 180r/min to obtain a copper ferrite sol-state mixture;
二、在95℃的温度条件下,以10mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续以180r/min的搅拌速率搅拌至铁酸铜溶胶态混合液蒸干,然后进行研磨,再置于马弗炉中,以3℃/min的升温速率升温至400℃,并在400℃的温度条件下煅烧8h,最后空冷至室温,研磨,得到铁酸铜/沸石尖晶石复合材料,所述的铁酸铜/沸石尖晶石复合材料上负载的铁酸铜尖晶石的粒径为2μm~30μm,所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:5。2. Under the temperature condition of 95℃, add natural zeolite powder to the copper ferrite sol mixture at a rate of 10mg/s, and continue to stir at a stirring rate of 180r/min until the copper ferrite sol mixture is evaporated to dryness. Then it was ground, placed in a muffle furnace, heated to 400°C at a heating rate of 3°C/min, and calcined at 400°C for 8 hours, finally cooled to room temperature in air, and ground to obtain copper ferrite/zeolite tip The copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material has a particle size of 2 μm to 30 μm, and the copper ferrite sol-state mixture contains the copper ferrite and natural zeolite The mass ratio of powder is 1:5.
步骤二中所述的天然沸石粉按以下步骤制备:取粒径一致的天然沸石,经高速粉碎机粉碎,然后依次用纯水和0.1mol/L盐酸清洗,得到天然沸石粉。The natural zeolite powder described in step two is prepared according to the following steps: natural zeolite with uniform particle size is taken, crushed by a high-speed pulverizer, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
对比试验:Comparative Test:
在20℃条件下,选择六个500mL的反应器(1#~6#):Under the condition of 20℃, select six 500mL reactors (1#~6#):
在1#反应器中,先加入超纯水和10mmol/L、PH为7的硼砂缓冲溶液,再以0.20g/L的比例加入实施例一中制备的铁酸铜/沸石尖晶石复合材料,最后加入2μmol/L的阿特拉津,通入臭氧的瞬间,反应开始计时,于0min、2min、5min、10min、20min、30min和40min分别取点。In the 1# reactor, first add ultrapure water and 10mmol/L borax buffer solution with a pH of 7, and then add the copper ferrite/zeolite spinel composite prepared in Example 1 at a ratio of 0.20g/L , And finally add 2μmol/L atrazine, the moment the ozone is introduced, the reaction starts timing, and take points at 0min, 2min, 5min, 10min, 20min, 30min and 40min respectively.
在2#反应器中,先加入超纯水和10mmol/L、PH为7的硼砂缓冲溶液,再以0.20g/L的比例加入实施例二中制备的铁酸铜/沸石尖晶石复合材料,最后加入2μmol/L的阿特拉津,通入臭氧的瞬间,反应开始计时,于0min、2min、5min、10min、20min、30min和40min分别取点。In the 2# reactor, first add ultrapure water and 10mmol/L borax buffer solution with a pH of 7, and then add the copper ferrite/zeolite spinel composite prepared in Example 2 at a ratio of 0.20g/L , And finally add 2μmol/L atrazine, the moment the ozone is introduced, the reaction starts timing, and take points at 0min, 2min, 5min, 10min, 20min, 30min and 40min respectively.
在3#反应器中,先加入超纯水和10mmol/L、PH为7的硼砂缓冲溶液,再以0.20g/L的比例加入实施例三中制备的铁酸铜/沸石尖晶石复合材料,最后加入2μmol/L的阿特拉津,通入臭氧的瞬间,反应开始计时,于0min、2min、5min、10min、20min、30min和40min分别取点。In the 3# reactor, first add ultrapure water and 10mmol/L borax buffer solution with a pH of 7, and then add the copper ferrite/zeolite spinel composite prepared in Example 3 at a ratio of 0.20g/L , And finally add 2μmol/L atrazine, the moment the ozone is introduced, the reaction starts timing, and take points at 0min, 2min, 5min, 10min, 20min, 30min and 40min respectively.
在4#反应器中,先加入超纯水和10mmol/L、PH为7的硼砂缓冲溶液,再以0.20g/L的比例加入天然沸石催化剂,最后加入2μmol/L的阿特拉津,通入臭氧的瞬间,反应开始计时,于0min、2min、5min、10min、20min、30min和40min分别取点。In the 4# reactor, first add ultrapure water and 10mmol/L borax buffer solution with a pH of 7, then add the natural zeolite catalyst at a ratio of 0.20g/L, and finally add 2μmol/L atrazine, At the moment of ozone entering, the reaction starts timing, and points are taken at 0min, 2min, 5min, 10min, 20min, 30min and 40min respectively.
在5#反应器中,先加入超纯水和10mmol/L、PH为7的硼砂缓冲溶液,再以0.20g/L的比例加入铁酸铜催化剂,最后加入2μmol/L的阿特拉津,通入臭氧的瞬间,反应开始计时,于0min、2min、5min、10min、20min、30min和40min分别取点。In the 5# reactor, first add ultrapure water and 10mmol/L borax buffer solution with a pH of 7, then add copper ferrite catalyst at a ratio of 0.20g/L, and finally add 2μmol/L atrazine. The moment the ozone is introduced, the reaction starts timing, and points are taken at 0min, 2min, 5min, 10min, 20min, 30min and 40min respectively.
在6#反应器中,先加入超纯水和10mmol/L、PH为7的硼砂缓冲溶液,然后加入2μmol/L的阿特拉津,通入臭氧的瞬间,反应开始计时,于0min、2min、5min、10min、20min、30min和40min分别取点。In the 6# reactor, first add ultrapure water and 10mmol/L borax buffer solution with a pH of 7, and then add 2μmol/L atrazine. The moment the ozone is introduced, the reaction starts timing, at 0min, 2min , 5min, 10min, 20min, 30min and 40min take points respectively.
图1为对比试验中,1#~6#反应器中阿特拉津的去除效率的对比图;如图1所示,同单独臭氧体系、单独天然沸石催化臭氧体系和单独铁酸铜催化臭氧体系相比,实施例一~实施例三制备的铁酸铜/沸石尖晶石复合材料显示了很高的催化活性,在反应时间为40分钟内,对水中的阿特拉津去除率较单独臭氧作用提升了约30%,而且其具有较高的化学稳定性,在反应后的水溶液中仅检测出微量铜铁离子的溶出,可以应用于实际水处理领域。而铁酸铜/沸石催化剂无明显的吸附作用;而单独使用臭氧氧化,只能降解少量阿特拉津;因此,实施例一~实施例三制备的铁酸铜/沸石尖晶石复合材料制作简单,成本低,操作简单,催化效率高。Figure 1 is a comparison diagram of the removal efficiency of atrazine in the 1#~6# reactor in the comparative test; as shown in Figure 1, it is the same as a single ozone system, a single natural zeolite catalyzed ozone system and a single copper ferrite catalyzed ozone Compared with the system, the copper ferrite/zeolite spinel composite materials prepared in Example 1 to Example 3 show very high catalytic activity. Within 40 minutes of reaction time, the removal rate of atrazine in water is relatively high. The effect of ozone is increased by about 30%, and it has high chemical stability. Only trace amounts of copper and iron ions are detected in the aqueous solution after the reaction, which can be used in the actual water treatment field. However, the copper ferrite/zeolite catalyst has no obvious adsorption effect; and the ozone oxidation alone can only degrade a small amount of atrazine; therefore, the copper ferrite/zeolite spinel composite material prepared in Examples 1 to 3 is made Simple, low cost, simple operation and high catalytic efficiency.
图2为实施例一制备的铁酸铜/沸石尖晶石复合材料,在0~120min内对水中阿特拉津的去除效率图;如图2所示,实施例一制备的铁酸铜/沸石尖晶石复合材料在120min时,将水中的阿特拉津完全降解。Figure 2 is a graph showing the removal efficiency of atrazine from water in the copper ferrite/zeolite spinel composite material prepared in Example 1 within 0 to 120 minutes; as shown in Figure 2, the copper ferrite/zeolite spinel composite material prepared in Example 1 The zeolite spinel composite material completely degrades the atrazine in the water at 120 minutes.
Claims (10)
- 铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于该制备方法按以下步骤完成:The preparation method of copper ferrite/zeolite spinel composite material is characterized in that the preparation method is completed in the following steps:一、在90℃~100℃的温度条件下,将硝酸铜和硝酸铁加入到无水乙醇中,搅拌均匀,然后加入无水柠檬酸,再搅拌均匀,得到铁酸铜溶胶态混合液,所述硝酸铜与硝酸铁的摩尔比为1:2,硝酸铜和硝酸铁的总物质的量与无水乙醇的体积的比为11.49mmol:(100mL~120mL),无水乙醇的体积与无水柠檬酸的物质的量的比为(100mL~120mL):7.66mmol;1. Under the temperature condition of 90℃~100℃, add copper nitrate and ferric nitrate to absolute ethanol, stir evenly, then add anhydrous citric acid, and stir evenly to obtain copper ferrite sol state mixture, so The molar ratio of copper nitrate to ferric nitrate is 1:2, the ratio of the total amount of copper nitrate and ferric nitrate to the volume of anhydrous ethanol is 11.49mmol: (100mL~120mL), the volume of anhydrous ethanol is relative to that of anhydrous ethanol. The ratio of the amount of citric acid is (100mL~120mL): 7.66mmol;二、在90℃~100℃的温度条件下,以10mg/s~20mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续搅拌至铁酸铜溶胶态混合液蒸干,然后进行研磨,再升温至400℃,并在400℃的温度条件下煅烧8h,最后空冷至室温,研磨,得到铁酸铜/沸石尖晶石复合材料,所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:(1~5)。2. Under the temperature condition of 90℃~100℃, add natural zeolite powder to the copper ferrite sol mixture at a rate of 10mg/s~20mg/s, and continue to stir until the copper ferrite sol mixture is evaporated to dryness. Then it was ground, heated to 400°C, and calcined at 400°C for 8 hours, and finally cooled to room temperature in air, and ground to obtain a copper ferrite/zeolite spinel composite material. The copper ferrite sol-state mixture contained iron The mass ratio of acid copper to natural zeolite powder is 1:(1~5).
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤一中所述在90℃~100℃的温度条件下,将硝酸铜和硝酸铁加入到无水乙醇中,以120r/min~180r/min的搅拌速率搅拌均匀。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, characterized in that in step 1, the copper nitrate and iron nitrate are added to the anhydrous under the temperature condition of 90°C to 100°C. In ethanol, stir evenly at a stirring rate of 120r/min to 180r/min.
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤一中所述加入无水柠檬酸,再以120r/min~180r/min的搅拌速率搅拌均匀,得到铁酸铜溶胶态混合液。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, characterized in that in step one, anhydrous citric acid is added, and then stirred evenly at a stirring rate of 120r/min to 180r/min, The copper ferrite sol state mixed liquid is obtained.
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤二中所述在90℃~100℃的温度条件下,以10mg/s~20mg/s的速率向铁酸铜溶胶态混合液中加入天然沸石粉,继续以120r/min~180r/min的搅拌速率搅拌至铁酸铜溶胶态混合液蒸干。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, characterized in that in step 2, under the temperature condition of 90°C to 100°C, at a rate of 10 mg/s to 20 mg/s Add natural zeolite powder to the copper ferrite sol state mixture, and continue to stir at a stirring rate of 120r/min to 180r/min until the copper ferrite sol state mixture is evaporated to dryness.
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤二中所述的天然沸石粉按以下步骤制备:取粒径一致的天然沸石,经高速粉碎机粉碎,然后依次用纯水和0.1mol/L盐酸清洗,得到天然沸石粉。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, characterized in that the natural zeolite powder described in step 2 is prepared by the following steps: natural zeolite with the same particle size is taken and passed through a high-speed pulverizer It is crushed, and then washed with pure water and 0.1 mol/L hydrochloric acid in sequence to obtain natural zeolite powder.
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤二中所述再以3℃/min的升温速率升温至400℃,并在400℃的温度条件下煅烧8h。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, characterized in that in step 2, the temperature is increased to 400°C at a heating rate of 3°C/min, and the temperature is 400°C. Calcined for 8h.
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤二中所述的铁酸铜/沸石尖晶石复合材料上负载的铁酸铜尖晶石的粒径为2μm~30μm。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, characterized in that the copper ferrite spinel supported on the copper ferrite/zeolite spinel composite material in step two is The particle size is 2 μm to 30 μm.
- 根据权利要求1所述的铁酸铜/沸石尖晶石复合材料的制备方法,其特征在于步骤二中所述铁酸铜溶胶态混合液中铁酸铜与天然沸石粉的质量比为1:1。The method for preparing copper ferrite/zeolite spinel composite material according to claim 1, wherein the mass ratio of copper ferrite to natural zeolite powder in the copper ferrite sol-state mixture in step two is 1:1 .
- 铁酸铜/沸石尖晶石复合材料的应用,其特征在于所述铁酸铜/沸石尖晶石复合材料作为催化剂,用于催化臭氧氧化降解水中的阿特拉津。The application of the copper ferrite/zeolite spinel composite material is characterized in that the copper ferrite/zeolite spinel composite material is used as a catalyst to catalyze ozone oxidation and degradation of atrazine in water.
- 根据权利要求9所述的铁酸铜/沸石尖晶石复合材料的应用,其特征在于所述铁酸铜/沸石尖晶石复合材料作为催化剂时,添加量为0.05g/L~1.0g/L。The application of the copper ferrite/zeolite spinel composite material according to claim 9, wherein when the copper ferrite/zeolite spinel composite material is used as a catalyst, the addition amount is 0.05g/L~1.0g/ L.
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CN115920889A (en) * | 2022-11-07 | 2023-04-07 | 上海交通大学 | Preparation and application of a foamy spinel catalyst |
CN116655442A (en) * | 2023-07-12 | 2023-08-29 | 西北大学 | A kind of titanium/copper ferrite microwave sensitive energetic material and its preparation method and application |
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CN111068739B (en) * | 2019-12-31 | 2022-01-25 | 哈尔滨工业大学 | Preparation method and application of copper ferrite/zeolite spinel composite material |
CN116786119A (en) * | 2023-04-18 | 2023-09-22 | 内蒙古大学 | A modified tourmaline/ferrite composite catalyst and its preparation method |
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CN116655442A (en) * | 2023-07-12 | 2023-08-29 | 西北大学 | A kind of titanium/copper ferrite microwave sensitive energetic material and its preparation method and application |
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